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Publication numberUS3905588 A
Publication typeGrant
Publication dateSep 16, 1975
Filing dateFeb 8, 1974
Priority dateFeb 8, 1974
Publication numberUS 3905588 A, US 3905588A, US-A-3905588, US3905588 A, US3905588A
InventorsLawrence Walter Reinhart
Original AssigneeCincinnati Milacron Inc
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method and apparatus for plasticating polymers
US 3905588 A
Abstract
A method and apparatus for plasticating highly crystalline polymers include a screw with a core and constant pitch thread with a thread outside diameter profile presenting or having a necked down or least diameter portion in its compression or central section and which when rotated within a constant diameter barrel provides a varying clearance between the screw and barrel whereby melt quality is improved and screw wear is reduced when such a polymer (for example: polypropylene and high density polyethylene) is passed therethrough.
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Description  (OCR text may contain errors)

' United States Patent [191 Reinhart [451 Sept. 16, 1975 METHOD AND APPARATUS FOR PLASTICATING POLYMERS [75] Inventor: Lawrence Walter Reinhart,

Loveland, Ohio Cincinnati Milacron Inc., Cincinnati, Ohio [22] Filed: Feb. 8, 1974 [21] Appl. N0.: 440,694

[73] Assignee:

[52] US. Cl 259/191; 259/10 [51] Int. Cl. B29B 1/10 [58] Field of Search 259/191, 193, 194, 192,

DIG. 1, DIG. 11; 416/176; 415/72; 425/207,

[56] References Cited UNITED STATES PATENTS 2,972,168 2/1961 Pastorello 425/209 3,263,276 8/1966 Maier 425/208 3,295,160 1/1967 Schippers 425/208 3,317,959 5/1967 List .l 259/191 3,727,892 4/1973 Notte et al 1 259/10 3,826,477 7/1974 Kunogi et a1. 259/191 Primary ExaminerI-Iarvey C. Hornsby Assistant ExaminerJames A. Niegowski Attorney, Agent, or FirmDaniel P. Worth [5 7] ABSTRACT 5 Claims, 2 Drawing Figures 10/ a w w '4 a e a 1 \x \\x \e\\ r\\ I k I /34 I34- 04 FEED COMPRESSION METERING SECTION SECTION SECTION 1% I27 I22 METHOD AND APPARATUS FOR PLASTICATING,

, POLYMERS I SUMMARY. AND [BACKGROUND This invention relates to an improved method and apparatus for plasticating polymers. One aspect relates to a method of plasticating highly crystalline polymers by passing same through a single screw type plasticator having a varying clearance between the screw-and barrel. An aspect relates to an improved screw having'an hourglass outside diameter profile. An aspect of the apparatusis to provide a single screw plasticator with such a screw mounted for rotation within a barrel havinga substantially constant inside diameter.

Processing highly crystalline thermoplastic aliphatic polymers such as polypropylene and high density polyethylene (specific gravity'equal or greater than 0.95) in a single screw plasticator generates a number of problems peculiar to these materials. For one thing the plastication is ordinarily accomplished by passing solid pellets of the polymer through a screw rotating within a heated barrel whereby mechanical and thermal energy are added to the plastic and change it from pelletized solid to a viscous-fluid. One of theproblems in handling these-materials is to plasticate the materials thoroughly andeliminate solid particles (unmelt) therein. Unfortunately these particular crystalline polymers do frequently provide melts of poor quality having a lot of solid particles in them, resulting in poor injection molding, extrusion, or what have you. Screw wear in the'single screw plasticatorsis also generally extreme and is characterized by wearing down the middle section of the screw by the flaking off of metal particles or the actual formationof flanges of inetalon thethread of the screw, the flanges being derived by metal being forced back'from its original position to form a sort of flange on the'trailing edge of the screw thread. On occasion screws worn in this fashion have actually produced higher quality melt than screws that have a straight or regular thread.

The present invention proposes to reduce the outside diameter of the screw in an area located between the ends of the thread or flight profile. This diametral change improves the quality of the melt and improves the overall quality of moldings produced from high density polyolefins. T g

In the prior art a typical screw for a single screw plasticator such as found'in extrusion machines for'making pipe or film or for plasticating materials prior to injection molding ordinarily'has a substantially constant outside thread (or flight) diameter and is divided into three sections along its length. The first section is a feed section for receiving pelletized solid plastic and having a small but substantially constant core diameter. Next in-lineis the compression section which receives materies thereof is Plastics Extrusion Technology and Therial from the feed section'and has an increasing core diameter. The third section is called a metering section. and is on the extreme downstream end of the screw and is characterized by having a constant core diameter etral clearance between the barrel and the screw flight.

Attempts to solve some of the problems of plasticap ing highly crystalline polymers in the past have involved various combinations of increasing the thermal ory by Gerhard Schenkel published in U.S. by American Elsevi'er Publishing Co., New York, NY Library of screw plasticators in providing a varying clearance preferably by providing a screw having the minimum outside diameter in a generally central region preferably in the compression section, which diameter increases'gradually to thatof the screw threads on the extrerne ends of the screw where preferably the diameters are substantially equal. Advantages in features of the instant construction permit easy replacement of a worn or ineffective (with high density polymers) screw, an improved melt quality, and minimum alterations to the machine cycle of operation which is especially important in the case of injection molding equipment.

Objects of the invention to provide an improved screw, an improved combination of barrel and screw, and/or an improved plasticating method.

Other objects, advantages and features will become apparent from the following specification when read in conjunction with the annexed drawings wherein:

FIG. 1 schematically illustrates a typical prior art injection molding machine in connection with which the invention will without prejudice be described by way of example but not limitation, such machine having a single screw plasticator with a heated barrel and screw, omitting ,details of injection molding machines not pertinent to the instant inventiomand FIG. 2 shows (in a different andsmaller scale than FIG. 1) a screw according to the present invention combined with the barrel of the FIG. 1 extruder.

The drawings are not .to scale.

FIG. 1 illustrates an injection molding machine 1 having a plasticating means 2 which receives solid pelletized highly crystalline polymers 3 in its feed hopper 4, plasticates same thereby changing it to a melt consisting of a highly viscous liquid which is then injected into a mold 5.

A plasticating means 2 includes a hydraulic motor 7 for rotating the screw 8 powered by pressurized hydraulicyliquid received fromthe pump 9 by means of a hydraulic control valve 10. The motor exhausts its hydraulic liquid .to a sump 11. A cycle controller 12 directs hydraulic fluid from the pump 9 to the motor and to the screw piston 14 by appropriately manipulating the motor-control valve 10 and piston control valve 16 in fashions well known to the prior art. Preferably the cycle controller adjusts'the cycle in response'to process conditions such as melt temperature l7, mold pressure 18 or injection velocity as indicated by electric tachometer 20 also as known to the art. Other control parameters can'be used those shown being by way of example not limitation; e-.=g., screw position can be used by having a position transducer (a potentiometer) 20 instead of a velocity measurement.-

A drive shaft 21 connected to the motor has a splined section 22 on which is mounted the hydraulic piston 14 that in turn slides within a hydraulic cylinder 23 that receives hydraulic .fluid by way of the control valve 16 and operates in a double acting fashion in order to advance or retract the screw. The piston 14 is connected to the splined section 22 by an internal splined section. The screw is directly connected to one end of the piston. It will be observed that the drive shaft, splined connection, piston, and screw provide a dual power train for rotating the screw 8 within the heated (with electric heaters 24) barrel 25 as well as for advancing and re tracting same whereby the screw can reciprocate in the barrel to inject plastic and duringplastication as is well known in the art.

The screw of FIG. 1 has a conventional prior art construction consisting of feed, compression and metering sections 26, 27, 28 arranged in series along the screw. A core 29 provides a support for the thread 30 which thread has a constant outside diameter and the barrel 25 in which it rotates likewise has a constant inside di ameter and there is a substantially constant clearance between the thread outside diameter and barrel inside diameter. The screw is integral, that is made from one piece of material. At the end of the screw is a tip assembly 31 which preferably has some sort of valve means in it to control back flow during injection strokes.

As illustrated in FIG. 1, and also as well known in the prior art, including the publications mentioned above, the feed section and metering section both have constant core diameters 32, 33 with the metering section having the larger core diameter. In the compression section the core diameter 35 increases as the structure proceeds from the feed to the metering section.

At the extreme end of the barrel is a nozzle 36 which is used as is well known to effectuate a passage of plasticated material from the barrel into the mold. I

In FIG. 2 is shown a barrel 125 (the barrel of FIG. 1 with the other details of FIG. 1 being understood as needed) containing a screw 108 constructed in accordance with the present invention. The screw is integral or made from one piece of material and is adapted for plasticating highly crystalline polymers. It may be flame hardened on the outside of the thread. The barrel, as explainedabove in connection with FIG. 1, has a substantially constant inside diameter and thereby provides a varying clearance 134 (meaning the space between the thread outside diameter and barrel inside diameter) that increases as the structure progresses from the feed to the central part of the compression section and thereafterdecreases. The thread outside diameter is preferably the same at the extreme ends of the feed and metering section; i.e., at the terminal thread helices whereby inserting the screw into a barrel is facilitated and also provides bearing surfaces at the extreme ends of the screw.

The extruder screw 108 of FIG. 2 has a core 129 with a thread 130 of preferably constant pitch that defines the feed compression and metering sections 126, 127, 128 as already stated; The core diameters 132, 133, l35 vary in the manner described in connection with FIG. .1; i.e., it is larger in the meteringthan in the feed section and increases as the screw core progresses through the compression section from the feed to the metering section. The screw 108 further comprises a thread having a varying outside diameter with such diameter being least in the compression section and with 4 the greatest outside diameters preferably being substantially equal and at the terminal ends of the thread in the feed and compression section whereby the thread has an hourglass outside diameter profile.

In its preferred embodiment, the thread 130 has a constant pitch, is used in a barrel having a substantially constant inside diameterand is made of one piece of material; i.e., in integral fashion.

The invention also embraces a combination of barrel and screw for plasticating highly crystalline polymers 3 where the structure comprises a varying radial or diametral clearance between the barrel and the outside diameter of the thread on the screw, the clearance being a maximum in a radial plane passing through the compression section and being at a minimum in respective radial planes at approximately where the thread terminates adjacent the opposite ends of the screw. At least one complete turn of the thread at each end is preferred for this maximum outside diameter to provide suitable bearing coaction between the thread and barrel.

The invention also embraces a method of plasticating highly crystalline polymers 3 such as polypropylene, or high density polyethylene (specific gravity equal to or greater than 0.95), mixtures thereof and copolymers thereof, or like materials by providing an apparatus 101 that includes a barrel in which is supported for rotation relative thereto a screw 108 having acore 129 and thread 130 that have in the order named, feed, compression and metering section. The method further incudes the steps of feeding into the apparatus adjacent the screw feed section as by means of the hopper at least one solid polymer of the class described, relatively rotating the said screw and said barrel by means ofthe hydraulic motor in the present embodiment the screw is turned within the barrel and as the material is plasticated it builds up between the screw tip assembly 31 or 131 (which preferably is a ball-check valve tip although a sleeve check valve tip may be used) and the nozzle and forces the screw to the rear until a volume of material ahead of the screw is great enough to makeup a shot for injection molding. The method further includes forcing in response to the relative rotation the polymer to pass through a passageway along the screw comprising varying radial clearance 134 between said thread on said screw and said barrel with the maximum such clearance being within the compression section 127 and the minimum such clearances being at the ends 126, 128 of the feed and metering sections and thereafter removing plasticated polymer through an opening such as the nozzle at the end of the barrel adjacent to the end of the screw metering section. v

Use of a screw manufactured to the described hourglass shape yields a reduced number of faulty moldings because'the melt quality is higher. Increased extruder RPM is not apparently required in order to maintain the throughput required for production purposes. The overall results from a production standpoint are that fewer rejected parts per unit of time are molded.

The invention claimed is:

1. An extruder'screw having a core and a thread thereon defining a feed section, compression section, and metering section wherein the core diameter is larger in the metering section than in the feed section and increases as the screw progresses through the compression section from the feed to the metering section that further comprises a thread having a varying outside diameter with the least such outside diameter being in the compression section and with its greatest outside diameters being substantially equal and at the ends of the thread in the feed and compression sections, whereby the thread has an hourglass outside diameter profile.

2. An extruder screw according to claim 1 wherein said thread has a constant pitch.

3. A single stage screw according to claim 1 that is integral or made from one piece of material adapted for plasticating highly crystalline polymers wherein the flight is flame hardened.

4. An extruder screw for a single screw extruder according to claim 1, combined with a barrel of substantially constant inside diameter in which said screw is rotatably mounted.

S. The combination in a single screw extruder for plasticating highly crystalline polymers of a barrel having a substantially constant inside diameter and threaded screw having feed, compression and metering sections the diameter of the core of which increases as the screw progresses through the compression from the feed to the metering section and which is supported within said barrel for rotation relative thereto, which combination further comprises: said thread having a varying outside diameter with the least such outside diameter being in the compression section and with its greatest outside diameters being substantially equal and at the end flights of the thread in the feed and metering sections, whereby the thread has an hourglass outside diameter profile and the combination is provided with a varying radial clearance between the inside diameter of the barrel and the thread on said screw with the greatest such clearance between the screw compression section and the adjacent portion of said barrel.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2972168 *Nov 6, 1957Feb 21, 1961Pastorello IgnazioMixing and thickening machine for extrusion
US3263276 *Oct 30, 1962Aug 2, 1966Richard MaierInjection molding machine
US3295160 *Jul 21, 1964Jan 3, 1967Barmag Barmer MaschfApparatus for spinning filaments of synthetic thermoplastic fiber-forming polymers
US3317959 *Oct 10, 1963May 9, 1967List HeinzMethod of extruding moldable material and screw type extruder
US3727892 *Dec 14, 1971Apr 17, 1973Usm CorpFeedback control for a continuous mixer having a control of internal pressure
US3826477 *Apr 10, 1972Jul 30, 1974Meiki Seisakusho KkInjection molding machine with a venting device
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4128341 *Apr 29, 1977Dec 5, 1978Ingersoll-Rand Co.Extruder screw
US4129386 *Jun 29, 1977Dec 12, 1978Akzona IncorporatedExtrusion apparatus
US4183673 *Nov 16, 1978Jan 15, 1980The Gillette CompanyMarbleization of plastic materials
US4357291 *Aug 28, 1980Nov 2, 1982Union Carbide CorporationDouble metering extruder screw and method of extrusion
US4798473 *Feb 15, 1985Jan 17, 1989Rauwendaal Christiaan JExtruder screw
US20110292756 *Feb 2, 2010Dec 1, 2011Hiroshi ShimizuHigh-shear melt-kneader and method of high shearing
EP0050496A2 *Oct 16, 1981Apr 28, 1982Union Carbide CorporationApparatus for extruding linear polyolefin materials having high viscosities
WO1997025407A1 *Dec 19, 1996Jul 17, 1997Henkel KgaaExtruder for producing washing and/or cleaning agents and process for resetting it_______________________________________________
Classifications
U.S. Classification366/88, 366/89, 264/349
International ClassificationB29C47/60, B29C45/60
Cooperative ClassificationB29C47/60, B29C45/60
European ClassificationB29C47/60, B29C45/60